Skin reactions to thimerosal and Leishmania in dogs from a leishmaniasis endemic area: it is better to keep them apart

Positive Montenegro's skin test is a delayed type hypersensitivity reaction widely used as indicative of previous infection with Leishmania in both humans and dogs. Montenegro's antigen consists of a crude Leishmania antigen solution, usually containing thimerosal as preserving agent. In this work it is shown that a large proportion of dogs (11 out of 56) examined in an endemic area of leishmaniasis presented induration at the site of injection of a diluent containing thimerosal alone. This clearly demonstrates that thimerosal leads to a high number of false positive skin reactions in dogs and that its use in Montenegro's skin test antigenic preparations should be avoided.

Vasopressin-dependent coupling between sodium transport and water flow in a mouse cortical collecting duct cell line.

Water balance is achieved through the ability of the kidney to control water reabsorption in the connecting tubule and the collecting duct. In a mouse cortical collecting duct cell line (mCCD(c11)), physiological concentrations of arginine vasopressin increased both electrogenic, amiloride-sensitive, epithelial sodium channel (ENaC)-mediated sodium transport measured by the short-circuit current (Isc) method and water flow (Jv apical to basal) measured by gravimetry with similar activation coefficient K(1/2) (6 and 12 pM, respectively). Jv increased linearly according to the osmotic gradient across the monolayer. A small but highly significant Jv was also measured under isoosmotic conditions. To test the coupling between sodium reabsorption and water flow, mCCD(c11) cells were treated for 24 h under isoosmotic condition with either diluent, amiloride, vasopressin or vasopressin and amiloride. Isc, Jv, and net chemical sodium fluxes were measured across the same monolayers. Around 30% of baseline and 50% of vasopressin-induced water flow is coupled to an amiloride-sensitive, ENaC-mediated, electrogenic sodium transport, whereas the remaining flow is coupled to an amiloride-insensitive, nonelectrogenic sodium transport mediated by an unknown electroneutral transporter. The mCCD(c11) cell line is a first example of a mammalian tight epithelium allowing quantitative study of the coupling between sodium and water transport. Our data are consistent with the 'near isoosmotic' fluid transport model.

Stable isotope geochemistry and phase-equilibria of coesite-bearing whiteschists, Dora Maira massif, Western Alps

Peak metamorphic temperatures for the coesite-pyrope-bearing whiteschists from the Dora Maira Massif, western Alps were determined with oxygen isotope thermometry. The deltaO-18(SMOW) values of the quartz (after coesite) (delta O-18 = 8.1 to 8.6 parts per thousand, n = 6), phengite (6.2 to 6.4 parts per thousand, n = 3), kyanite (6.1 parts per thousand, n = 2), garnet (5.5 to 5.8 parts per thousand, n = 9), ellenbergerite (6.3 parts per thousand, n = 1) and rutile (3.3. to 3.6 parts per thousand, n = 3) reflect isotopic equilibrium. Temperature estimates based on quartz-garnet-rutile fractionation are 700-750-degrees-C. Minimum pressures are 31-32 kb based on the pressure-sensitive reaction pyrope + coesite = kyanite + enstatite. In order to stabilize pyrope and coesite by the temperature-sensitive dehydration reaction talc + kyanite = pyrope + coesite + H2O, the a(H2O) must be reduced to 0.4-0.75 at 700 750-degrees-C. The reduced a(H2O) cannot be due to dilution by CO2, as pyrope is not stable at X (CO2) > 0.02 (T = 750-degrees-C; P = 30 kb). In the absence of a more exotic fluid diluent (e.g. CH4 or N2), a melt phase is required. Granite solidus temperatures are approximately 680-degrees-C/30 kb at a(H2O) = 1.0 and are calculated to be approximately 70-degrees-C higher at a(H2O) = 0.7, consistent with this hypothesis. Kyanite-jadeite-quartz bands may represent a relict melt phase. Peak P-T-f(H2O) estimates for the whiteschist are 34 +/- 2 kb, 700-750-degrees-C and 0.4-0.75. The oxygen isotope fractionation between quartz (deltaO-18 = 11.6%.) and garnet (deltaO-18 = 8.7 parts per thousand) in the surrounding orthognesiss is identical to that in the coesite-bearing unit, suggesting that the two units shared a common, final metamorphic history. Hydrogen isotope measurements were made on primary talc and phengite (deltaD(smow) = -27 to -32 parts per thousand), on secondary talc and chlorite after pyrope (deltaD = - 39 to - 44 parts per thousand) and on the surrounding biotite (deltaD = -64 parts per thousand) and phengite (deltaD = -44 parts per thousand) gneiss. All phases appear to be in near-equilibrium. The very high deltaD values for the primary hydrous phases is consistent with an initial oceanic-derived/connate fluid source. The fluid source for the retrograde talc + chlorite after pyrope may be fluids evolved locally during retrograde melt crystallization. The similar deltaD, but dissimilar deltaO-18 values of the coesite-bearing whiteschists and hosting orthogneiss suggest that the two were in hydrogen isotope equilibrium, but not oxygen isotope equilibrium. The unusual hydrogen and oxygen isotope compositions of the coesite-bearing unit can be explained as the result of metasomatism from slab-derived fluids at depth.

Laimentimen merkitys metallien neste-nesteuutossa

Työssä tutkittiin korkean leimahduspisteen laimentimien vaikutusta uuton tehokkuuteen ja turvallisuuteen. Kirjallisuusosa sisältää katsauksen uuttolaitoksilla tapahtuneista suuronnettomuuksista, staattisen sähkön aiheuttamista vaaroista uuttolaitoksilla ja kaupallisesti saatavista laimentimista. Lisäksi kirjallisuusosassa tarkastellaan hiilivetyjen molekyylirakenteen vaikutusta niiden leimahduspisteeseen, haihtuvuuteen, viskositeettiin ja liuotinominaisuuksiin. Kokeellisessa osassa tutkittiin uuton tehokkuutta kuvaavia ominaisuuksia, joita olivat sekoituksen pisarakoko, faasien selkeytymisnopeus,uuton ja takaisinuuton kinetiikka, orgaanisen faasin viskositeetti ja tiheys. Uuttoliuosten turvallisuusominaisuuksia tutkittiin mittaamalla synteettisten uuttoliuosten ja laimentimien leimahduspisteitä sekä sähköisesti varattujen laimentimien relaksaatioaikoja. Korkean leimahduspisteen laimentimena käytettiin Orfom SX 11-laimenninta. Vertailukohteena käytettiin Shellsol D70- ja Escaid 100- laimentimia. Malliuuttona käytettiin kuparin uuttoa hydroksioksiimireagensilla happamasta sulfaattiliuoksesta. Kokeissa havaittiin, että korkean leimahduspisteen laimentimen viskositeetti oli huomattavasti suurempi kuin Shellsol D70- laimentimella. Korkea viskositeetti hidasti faasien selkeytymistä uutossa, mutta sillä ei ollut vaikutusta uuton kinetiikkaan tai sekoituksen aiheuttamaan pisarakokoon. Uuttoliuoksen reagenssipitoisuudella havaittiin olevan vaikutusta uuttoliuoksen leimahduspisteeseen, mutta uuttoliuoksen latausasteella ei havaittu olevan vaikutusta. Sähköisesti varattujen laimentimien varauksien relaksaatioajoissa oli hieman eroja, mutta relaksaatioajat olivat kaikilla laimentimilla liian pitkiä staattisen sähkön aiheuttaman vaaran poistamiseksi.

Kuparinuuttoliuosten adsorptiopuhdistus

Työssä tutkittiin laboratorio-olosuhteissa yhdeksän eri adsorbentin sopivuutta kuparinuuttoliuosten adsorptiopuhdistukseen eli savikäsittelyyn. Tarkoituksena oli poistaa uuttoliuoksesta laimentimen ja reagenssin hapettumis- ja hajoamistuotteita. Adsorbenttien sopivuus uuttoliuosten puhdistukseen määritettiin adsorptio-, kinetiikka- ja faasien selkeytymisaikakokeilla. Tehdyissä kokeissa käytettiin sekä hapetettua synteettistä uuttoliuosta että teollisuudesta saatuja autenttisia kuparinuuttoliuoksia. Uuttoreagenssit olivat hydroksi-oksiimeihin perustuvia. Teollisuudesta saaduista käytetyistä adsorbenteista eluoidun liuoksen kaasugromatografi- ja massaspektrometrianalyysissä ei havaittu selviä merkkejä reagenssin tai laimentimen hajoamistuotteista. Savikäsittely lyhensi faasien selkeytymisaikaa merkittävästi. Bentoniittipohjaisten savien havaittiin soveltuvan parhaiten uuttoliuosten adsorptiopuhdistukseen. IR-analyysin perusteella niiden pinnalle adsorboitui myös eniten karbonyyliryhmiä sisältäviä yhdisteitä. Faasien selkeytymisajan havaittiin huonontuvan itsestään liuosten seistessä savikäsittelyn jälkeen. Noin vuorokauden jälkeen selkeytymisaika tasaantui tasolle, joka oli kuitenkin huomattavasti parempi kuin käsittelemättömällä liuoksella. Savikäsittelyssä käytettävän saven optimimäärä oli noin 1 p-%:a ja sekoitusaika muutamia minuutteja. Savikäsittelyllä ei ollut merkittävää vaikutusta kuparinuuton kinetiikkaan. Työssä tutkittiin laboratorio-olosuhteissa yhdeksän eri adsorbentin sopivuutta kuparinuuttoliuosten adsorptiopuhdistukseen eli savikäsittelyyn. Tarkoituksena oli poistaa uuttoliuoksesta laimentimen ja reagenssin hapettumis- ja hajoamistuotteita. Adsorbe

Nikkelin takaisinuutto karboksyylihappoon perustuvasta uuttoreagenssista

Työssä tutkittiin typpihapon soveltuvuutta nikkelin takaisinuuttoon. Tarkoituksena oli selvittää, millä typpihapon konsentraatioilla orgaaninen faasi, joka koostuu Versatic 10 uuttoreagenssista ja alifaattisesta laimentimesta, alkaa nitrautua tai hapettua ja mitkä ovat mahdolliset sivureaktiot. Lisäksi tutkittiin rikkihapon ja eräiden orgaanisten aineiden kontaminaation vaikutusta uuttoliuokseen. Kirjallisuusosassa kartoitetaan mahdollisten nitrautumisreaktioiden mekanismit, sekä kuvataan laimentimen, uuttoreagenssin ja mahdollisten reaktiotuotteiden ominaisuuksia, sekä niiden mahdollisessa muodostumisessa syntyviä riskejä. Orgaanisen faasin kestotesteissä tutkittavia muuttujia olivat typpi- ja rikkihapon konsentraatio, sekoitusaika, lämpötila, avoin tai suljettu astia sekä vieraiden aineiden kontaminaatio. Kontaminaatiota aiheuttavien orgaanisten materiaalien funktionaaliset ryhmät olivat hydroksi-, karbonyyli- ja amiiniryhmät, joiden lisäksi tutkittiin syklisen yhdisteen kontaminaatiota. Analyyseissä käytettiin FT-IR- spektroskopiaa, jolla tutkittiin reagenssin funktionaalisen ryhmän reaktioita ja uusien ryhmien muodostumista, sekä seurattiin selkeytyksessä erottumattomien typpiyhdisteiden määrää ja laatua orgaanisessa faasissa. Uuttofaasin koostumuksen muutosta seurattiin myös mittaamalla leimahduspisteen muutosta.

Qualitative, quantitative and temporal study of cutting agents for cocaine and heroin over 9 years

Forensic laboratories mainly focus on the qualification and the quantitation of the illicit drug under analysis as both aspects are used for judiciary purposes. Therefore, information related to cutting agents (adulterants and diluents) detected in illicit drugs is limited in the forensic literature. This article discusses the type and frequency of adulterants and diluents detected in more than 6000 cocaine specimens and 3000 heroin specimens, confiscated in western Switzerland from 2006 to 2014. The results show a homogeneous and quite unchanging adulteration for heroin, while for cocaine it could be characterised as heterogeneous and relatively dynamic. Furthermore, the results indicate that dilution affects more cocaine than heroin. Therefore, the results provided by this study tend to reveal differences between the respective structures of production or distribution of cocaine and heroin. This research seeks to promote the systematic analysis of cutting agents by forensic laboratories. Collecting and processing data related to the presence of cutting agents in illicit drug specimens produces relevant information to understand and to compare the structure of illicit drug markets.

The cutting of cocaine and heroin: a critical review

The illicit drug cutting represents a complex problem that requires the sharing of knowledge from addiction studies, toxicology, criminology and criminalistics. Therefore, cutting is not well known by the forensic community. Thus, this review aims at deciphering the different aspects of cutting, by gathering information mainly from criminology and criminalistics. It tackles essentially specificities of cocaine and heroin cutting. The article presents the detected cutting agents (adulterants and diluents), their evolution in time and space and the analytical methodology implemented by forensic laboratories. Furthermore, it discusses when, in the history of the illicit drug, cutting may take place. Moreover, researches studying how much cutting occurs in the country of destination are analysed. Lastly, the reasons for cutting are addressed. According to the literature, adulterants are added during production of the illicit drug or at a relatively high level of its distribution chain (e.g. before the product arrives in the country of destination or just after its importation in the latter). Their addition seems hardly justified by the only desire to increase profits or to harm consumers' health. Instead, adulteration would be performed to enhance or to mimic the illicit drug effects or to facilitate administration of the drug. Nowadays, caffeine, diltiazem, hydroxyzine, levamisole, lidocaïne and phenacetin are frequently detected in cocaine specimens, while paracetamol and caffeine are almost exclusively identified in heroin specimens. This may reveal differences in the respective structures of production and/or distribution of cocaine and heroin. As the relevant information about cutting is spread across different scientific fields, a close collaboration should be set up to collect essential and unified data to improve knowledge and provide information for monitoring, control and harm reduction purposes. More research, on several areas of investigation, should be carried out to gather relevant information.

Estudo da influência do diluente reativo PGE na cinética de cura de resina epóxi utilizada em compósitos estruturais

Phenil glycidyl ether (PGE), a monofunctional diluent, has been used in epoxy resins formulations in order to increase the toughness of the epoxy molded composite. In a systematic study concerning its influence in the cure kinetics of the epoxy resin, it was used in concentrations of 2,5; 5,0; 10 and 20% in relation to a diglycidyl ether bisphenol-A (DGEBA)/diamino diphenil-sulfone (DDS) base matrix. Dynamic and isothermal scanning analysis were carried out using a differential scanning calorimety (DSC) equipment. For all the concentrations of PGE, a n order kinetics was observed, with n varing between 0,35 -- 0,91 as a function of the increase in the PGE concentration.

Reagenssin pinta-aktiivisuuden hyödyntäminen sinkin uutossa

Työssä tutkittiin sinkin uutossa käytettävän di(2-etyyliheksyyli)fosforihappo (D2EHPA) -uuttoreagenssin faasikäyttäytymistä ja miten laimentimen koostumus, lämpötila ja orgaanisen faasin sinkkipitoisuus vaikuttavat faasitasapainoon. Laimentimen vaikutuksen havaittiin olevan pientä, kun taas lämpötilan nostaminen yli huoneenlämpötilan leventää faasidiagrammin yksifaasialuetta. Pienet orgaanisen faasin sinkkipitoisuudet eivät juuri vaikuta faasitasapainoon. Sinkin ja D2EHPA:n moolisuhteen ollessa välillä 0,1–0,2 kompleksin rakenne ilmeisesti muuttuu. Sinkkipitoisuuden kasvaessa yksifaasialue muodostuu pienemmillä ammoniakkimäärillä. Suurilla orgaanisen faasin sinkkipitoisuuksilla ja ammoniakkimäärillä muodostuu orgaanisen faasin ja vesifaasin välille kolmas nestefaasi. D2EHPA:n (40 p %) vesipitoisuuden ja viskositeetin pH riippuvuutta tutkittiin, kun laimentimena oli alifaattinen hiilivetyliuotin. Nostettaessa pH yli 3,5:n uuttoreagenssi alkoi muodostaa käänteismisellejä, jolloin orgaanisen faasin vesipitoisuus ja viskositeetti kasvoivat eksponentiaalisesti. Sinkin mukana uuttautuu epäpuhtauksia kuten Al3+, Co2+, Cu2+, Na+, Ni2+, Cl- ja F-. Takaisinuuton kautta epäpuhtaudet joutuvat talteenottoelektrolyysiin, jossa ne voivat vaikuttaa tuotteen laatuun ja laskea virtahyötysuhdetta. Tarkoituksena oli tutkia väheneekö epäpuhtauksien myötäuuttautuminen jollakin tietyllä sinkin latausasteella. Fluoridin ja kuparin uuttautumisen havaittiin vähenevän vasta, kun sinkin pitoisuus orgaanisessa faasissa oli yli 20 g/L lämpötilasta riippumatta. Fluoridi uuttautuu mahdollisesti alumiinikompleksina ja/tai fluorihappona. Koboltin ja nikkelin myötäuuttautumisen havaittiin vähenevän, kun sinkin latausaste oli yli 10 g/L. Natrium ja kloridi eivät myötäuuttautuneet.

The Role of Surfactant Properties of Extractants in Hydrometallurgical LiquidLiquid Extraction Processes

The amphiphilic nature of metal extractants causes the formation of micelles and other microscopic aggregates when in contact with water and an organic diluent. These phenomena and their effects on metal extraction were studied using carboxylic acid (Versatic 10) and organophosphorus acid (Cyanex 272) based extractants. Special emphasis was laid on the study of phase behaviour in a pre neutralisation stage when the extractant is transformed to a sodium or ammonium salt form. The pre neutralised extractants were used to extract nickel and to separate cobalt and nickel. Phase diagrams corresponding to the pre neutralisation stage in a metal extraction process were determined. The maximal solubilisation of the components in the system water(NH3)/extractant/isooctane takes place when the molar ratio between the ammonia salt form and the free form of the extractant is 0.5 for the carboxylic acid and 1 for the organophosphorus acid extractant. These values correspond to the complex stoichiometry of NH4A•HA and NIi4A, respectively. When such a solution is contacted with water a microemulsion is formed. If the aqueous phase contains also metal ions (e.g. Ni²+), complexation will take place on the microscopic interface of the micellar aggregates. Experimental evidence showing that the initial stage of nickel extraction with pre neutralised Versatic 10 is a fast pseudohomogeneous reaction was obtained. About 90% of the metal were extracted in the first 15 s after the initial contact. For nickel extraction with pre neutralised Versatic 10 it was found that the highest metal loading and the lowest residual ammonia and water contents in the organic phase are achieved when the feeds are balanced so that the stoichiometry is 2NH4+(org) = Nit2+(aq). In the case of Co/Ni separation using pre neutralised Cyanex 272 the highest separation is achieved when the Co/extractant molar ratio in the feeds is 1 : 4 and at the same time the optimal degree of neutralisation of the Cyanex 272 is about 50%. The adsorption of the extractants on solid surfaces may cause accumulation of solid fine particles at the interface between the aqueous and organic phases in metal extraction processes. Copper extraction processes are known to suffer of this problem. Experiments were carried out using model silica and mica particles. It was found that high copper loading, aromacity of the diluent, modification agents and the presence of aqueous phase decrease the adsorption of the hydroxyoxime on silica surfaces.

Recovery of carboxylic acids from aqueous streams by extraction and back extraction

Separation of carboxylic acids from aqueous streams is an important part of their manufacturing process. The aqueous solutions are usually dilute containing less than 10 % acids. Separation by distillation is difficult as the boiling points of acids are only marginally higher than that of water. Because of this distillation is not only difficult but also expensive due to the evaporation of large amounts of water. Carboxylic acids have traditionally been precipitated as calcium salts. The yields of these processes are usually relatively low and the chemical costs high. Especially the decomposition of calcium salts with sulfuric acid produces large amounts of calcium sulfate sludge. Solvent extraction has been studied as an alternative method for recovery of carboxylic acids. Solvent extraction is based on mixing of two immiscible liquids and the transfer of the wanted components form one liquid to another due to equilibrium difference. In the case of carboxylic acids, the acids are transferred from aqueous phase to organic solvent due to physical and chemical interactions. The acids and the extractant form complexes which are soluble in the organic phase. The extraction efficiency is affected by many factors, for instance initial acid concentration, type and concentration of the extractant, pH, temperature and extraction time. In this paper, the effects of initial acid concentration, type of extractant and temperature on extraction efficiency were studied. As carboxylic acids are usually the products of the processes, they are wanted to be recovered. Hence the acids have to be removed from the organic phase after the extraction. The removal of acids from the organic phase also regenerates the extractant which can be then recycled in the process. The regeneration of the extractant was studied by back-extracting i.e. stripping the acids form the organic solution into diluent sodium hydroxide solution. In the solvent regeneration, the regenerability of different extractants and the effect of initial acid concentration and temperature were studied.

Physicochemical study of CaCO3 from egg shells

Calcium carbonate, a pharmaceutical excipient, is widely used as diluent in solid dosage forms. It is also used as a base for medicinal and dental preparations, a buffering and dissolution aid for dispersible tablets, a food additive and a calcium supplement. Egg shells are a rich source of mineral salts, mainly calcium carbonate, which corresponds to about 94% of the shell. Layer farms produce large amounts of shells, whose final disposal poses a challenge from the environmental standpoint. This work was designed to evaluate the physicochemical and thermal properties of calcium carbonate obtained from egg shells. The findings indicated that calcium carbonate from egg shells can be used as an alternative pharmaceutical excipient.

Le réengagement du Canada dans les Amériques : déficits démocratiques, intégration économique et insécurité

En 2007, le premier ministre Stephen Harper a annoncé que le renouvellement de l’engagement du Canada dans les Amériques était une priorité internationale pour son gouvernement. Le document qui a formalisé la nouvelle priorité accordée à l’hémisphère occidental stipule que le Canada s’est engagé à faire progresser concurremment la démocratie, l’intégration économique et la sécurité. Cette recherche a pour but de remettre en cause le discours officiel en analysant la politique du Canada à l’égard de la Colombie et du Honduras. L’étude sur le cas colombien porte sur les effets de l’intégration économique sur les droits humains et la sécurité. Elle montre que le texte de l’accord de libre-échange Canada-Colombie et les évaluations d’impact sur les droits humains n’abordent pas convenablement les risques entourant les investissements canadiens et que leurs lacunes diluent l’engagement d’Ottawa envers la protection des droits humains et la résolution du conflit. L’étude sur le cas hondurien porte sur l’impact des déficits démocratiques et de l’insécurité sur l’intégration économique. Elle montre que le virage à droite qui a suivi le coup d’État de 2009 a permis au gouvernement canadien d’entreprendre des négociations de libre-échange bilatérales et de prendre part à la réforme du code minier du Honduras, tandis que les déficits démocratiques et l’insécurité ont empêché la population hondurienne de participer d’une manière significative au processus d’intégration économique. Nous concluons que ces deux cas contredisent le discours officiel dans la mesure où l’objectif de l’intégration économique a été atteint aux dépens des autres objectifs.

IR spectrum and radiative forcing of CF4 revisited

Carbon tetrafluoride (CF4) is included as a greenhouse gas within the Kyoto Protocol. There are significant discrepancies in the reported integrated infrared (IR) absorption cross section of CF4 leading to uncertainty in its contribution to climate change. To reduce this uncertainty, the IR spectrum of CF4 was measured in two different laboratories, in 0 933 hPa of air diluent at 296 +/- 2K over the wavelength range 600-3700 cm(-1) using spectral resolutions of 0.03 or 0.50 cm(-1). There was no discernable effect of diluent gas pressure or spectral resolution on the integrated IR absorption, and a value of the integrated absorption cross section of (1.90 +/- 0.17) x 10(-16) cm(2) molecule(-1) cm(-1) was derived. The radiative efficiency (radiative forcing per ppbv) and GWP (relative to CO2) of CF4 were calculated to be 0.102 W m(-2) ppbv(-1) and 7200 (100 year time horizon). The GWP for CF4 calculated herein is approximately 30% greater than that given by the Intergovernmental Panel on Climate Change (IPCC) [ 2002] partly due to what we believe to be an erroneously low value for the IR absorption strength of CF4 assumed in the calculations adopted by the IPCC. The radiative efficiency of CF4 is predicted to decrease by up to 40% as the CF4 forcing starts to saturate and overlapping absorption by CH4, H2O, and N2O in the atmosphere increases over the period 1750-2100. The radiative forcing attributable to increased CF4 levels in the atmosphere from 1750 to 2000 is estimated to be 0.004 W m(-2) and is predicted to be up to 0.033 W m(-2) from 2000 to 2100, dependent on the scenario.